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RECOVERY OF RARE EARTHS AND SCANDIUM FROM URANIUM LEACHATES
Ural Federal University
Physical Technology Institute
The Department of Rare Metals and Nanomaterials
SCALE Scandium-Inventory Workshop – 27/11/2018
Ural Federal University
Today:
• Top 500-550 in QS World University Ranking
• Top 10 in Interfax Russian national ranking
• The 4th among Russian universities by the
number of the articles published in
internationally recognized
scientific journals
UrFU is situated on the border of Europe and Asia
Institute of Physics and
Technology (PhysTech)
Research Priorities:
• Chemistry of Rare and Radioactive Elements
• Atomic Eneregtics Modernization (research of a
closed fuel cycle with salt and metal melts based
generators of 4th generation)
• Nanomaterials for Solar and Hydrogen Energy
• Radiopharmaceuticals for Cancer Diagnostics and
Therapy
The border between Europe and Asia
The technology of recovery REE and scandium as by-products to
uranium ISL
The technology of extraction REE from apatite and
phosphogypsum
Main recent achievements
JSC Dalur is located in the Dalmatovsky District of Russia’sKurgan Region. The company conducts commercial development of deposits in the Trans-Ural Uranium-Ore Area (Dalmatovskoye and Khokhlovskoye). JSC Dalur produces uranium by downhole in-situ leaching method.The company’s finished product is concentrate of natural
uranium (yellow cake).
Concentrations:
•REE– 30 mg/l
•Sc – 0.8 mg/l
JSC Khiagda is located in the Bauntovsky District of the Republic of Buryatia. The company develops the deposits of the Khiagdinskoye ore field.Test uranium mining with the use of in-situ leaching method began in 1999.Productive solutions are processed into the end product —concentrate of natural uranium (yellow cake).
Concentrations:
•REE – 60 mg/l
•Sc – 0.5 mg/l
LREE HREE
70 30
LREE HREE
70 30
The distribution of lanthanides in solution ISL uranium The distribution of lanthanides in solution ISL uranium
10-15% scandium oxide concentrate and 85-90% REE concentrateCarbonate REE concentrate and its activity rate
№ Element , % № Element , %
1 Li 0,0007 26 Zr 0,0083
2 Be 0,0029 27 La 7,7836
3 B 0,0203 28 Ce 22,3859
4 Na 0,2442 29 Pr 3,3187
5 Mg 0,0536 30 Nd 11,6157
6 Al 0,6719 31 Sm 1,9142
7 P 0,1306 32 Eu 0,4196
8 K 0,0583 33 Gd 2,4324
9 Ca 0,2452 34 Tb 0,2170
10 Sc 0,0202 35 Dy 2,7096
11 Ti 0,0022 36 Ho 0,0713
12 V 0,0005 37 Er 0,1224
13 Cr 0,0084 38 Tm 0,0060
14 Mn 0,0086 39 Yb 0,0476
15 Fe 0,0885 40 Lu 0,0059
16 Co 0,0003 41 Th 0,0004
17 Ni 0,0044 42 U 0,0084
18 Cu 0,0051 43 Σ REE 54,2757
19 Zn 0,0436
activity concentration 5,8±0,9·106
Bq kg-1
20 Ga 0,0207
21 Ge 0,0331
22 Se 0,4656
23 Rb 0,0002
24 Sr 0,0012
25 Y 1,2257
REE concentrate activity is basically caused by Ac-227 and its decay products.
- It occurs in uranium and thorium ores
- One tone of natural uranium contains only 6*10-5 gram of actinium
- To produce 1 gram of actinium you need to recycle 16,000 tons of uranium, (or 1000 wagons)
Uranium-235 decay chain
Methods of REE and Ac separation
Chromatographic actinium separation
from REE:
It is based on the ionic radius difference
For this aim complexation ionic exchange chromatography is used with organic acid or salts solutions (citrates, lactates, etc) as eluents
In this case Actinium is eluted last
Actinium has a similar chemical behavior as REE (La, Ce and others)
Extraction method of actinium separation
from REE :
It is based on the extraction coefficients difference
Tributyl phosphate (TBP, phosphoric acid ester) (C4H9O) 3P = O is used to remove Actinium from low pH solutions in a significant amounts of salting-out agents presence (ammonium nitrate, aluminum and others)
Also TTA (tetradecylthioacetic acid) is used to separate actinium from radium and its decay products as TBP
REE recovery mini-pilot test
Developed deactivation technology was tested
under industrial conditions at the uranium
mining plant. Approximately 100 g of the REE’s
concentrate with high activity was treated;
after deactivating it was about 90 g of REE’s
concentrate with activity concentration of
(1-5) × 103 Bq kg-1.
Uranium sorption column 50 m3
REE deactivation column 15 dm3
Prospective industrial sources of scandium in Russia
Source Sc content
Uranium leach liquors (ULL) <1 mg/l
Hydrolytic waste acid after production of TiO2 ~20 mg/l
Red mud (bauxite treatment waste) 0.007–0.011%
Coal ash 0.006-0.012 %
Uranium ores Up to 0.002%
Tungsten ores 0.01–0.1%
Ion exchange resins for preliminary scandium separation
Purolite S-950
Lewatit TP-260
Tulsion CH-93
ЭКО-10
Aminomethyl phosphonic ampholytes
Polyfunctional ion exchange resin
Purolite S-957
Characteristics of Sc sorption from ULL by various IEX Resins
Element Sc Th Al Fe Ti U
Capacity, mg per g of resin
0.28 0.58 7.41 3.21 1.38 0.38
Full dynamic exchange capacity
Tulsion CH 93
ElementAl Ca Sc Fe Th U
Capacity, mg per g of resin
26.43 4.5 0.65 60.67 1.09 0.43
Purolite S-957
The dynamics of Sc sorption
Dynamics of elements sorption by Purolite S-957
Kd Sc/Th=1.14
Kd Sc/Th=1.41
Characteristics of Sc sorption from ULL by various IEX Resins
Purolite АА-03 Dynamics of elements sorption by Purolite АА-03
IR spectra of Purolite S-957, S-950 and АА-03
in H+ form
IR spectra of Purolite S-957, S-950 and АА-03
in Sc3+ form
Element Al Ca Sc Fe Th UCapacity,
mg per g of resin
10.14 0.27 0.37 15.47 0.14 0.44
0
0,2
0,4
0,6
0,8
1
1,2
1,4
0 20 40 60 80 100 120
С/С
0
V/Vкол
Al
Ca
Sc
Fe
Y
Mo
Th
U
Ti
Kd Sc/Th=6.28
40
0
60
0
80
0
10
00
12
00
14
00
16
00
Пр
оп
уска
ни
е, %
V, см-1
S-957
S-950
AA-03
40
0
60
0
80
0
10
00
12
00
14
00
16
00
Пр
оп
уска
ни
е, %
V, см-1
S-957
S-950
AA-03
Radioactive contaminants in the primary scandium concentrate
0
3000
6000
9000
12000
15000
18000
0 50 100 150 200 250 300 350 400 450 500
E, keV
Co
un
ts
0
10
20
30
40
50
60
70
80
2000 3000 4000 5000 6000 7000 8000
Co
un
ts
Е, keV
Gamma spectrum of the Sc concentrate Alpha spectrum of the Sc concentrate
Radioactivity of the Sc concentrate is conditioned by presence thorium-234 (half-life is 24
days, beta and gamma emitter) and thorium-230 (half-life is 80,000 years, pure alpha
emitter). Activity was up to 108 - 1011 Bq/kg depending on the resin type being used for
scandium separation.
Sc/Th separation is necessary
Scandium recovery mini-pilot test
The results of work of the mini-pilot test
Compound % wt. Compound % wt.Sc 30.09 Cl 0.063Na 9.61 K 0.049Al 3.29 Sr 0.007
Mg 0.78 P 0.005Ca 0.65 Y 0.004Fe 0.12 Zr 0.003Si 0.08 Th 0.003S 0.070 Ni 0.001
Composition of the scandium concentrate obtained at the mini-pilot test
Scandium recovery pilot scale plant (200 m3 of ULL per hour)
The results of work of the pilot scale plant
Composition of the scandium concentrate obtained at the pilot scale plant
Compound % wt. Compound % wt.ScF3 98.040 Y2O3 0.037FeF2 0.395 CeO2 0.009SO3 0.355 Pr6O11 0.006NaF 0.340 Nd2O3 0.004AlF3 0.298 V2O5 0.003
Si 0.131 ThO2 0.002C 0.085 ZrO2 0.002
MgF2 0.080 SrO 0.002CaF2 0.058
Vielen Dank für Ihre Aufmerksamkeit!
Thanks for Attention!